CN112128977A - Process method for heating pretreatment of hazardous waste barreled material - Google Patents
Process method for heating pretreatment of hazardous waste barreled material Download PDFInfo
- Publication number
- CN112128977A CN112128977A CN202011138612.9A CN202011138612A CN112128977A CN 112128977 A CN112128977 A CN 112128977A CN 202011138612 A CN202011138612 A CN 202011138612A CN 112128977 A CN112128977 A CN 112128977A
- Authority
- CN
- China
- Prior art keywords
- heating
- materials
- barreled
- hazardous waste
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H7/00—Storage heaters, i.e. heaters in which the energy is stored as heat in masses for subsequent release
- F24H7/02—Storage heaters, i.e. heaters in which the energy is stored as heat in masses for subsequent release the released heat being conveyed to a transfer fluid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B15/00—Preventing escape of dirt or fumes from the area where they are produced; Collecting or removing dirt or fumes from that area
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention provides a process method for heating pretreatment of hazardous waste barreled materials, which comprises the following steps: (1) according to the complexity of barreled hazardous waste materials, processing according to batches, opening a barrel cover before heating, and putting the barrel cover into a heating box; (2) determining a proper heating temperature according to the early-stage material analysis condition, and opening an internal circulating fan and an overflow valve simultaneously after the material is heated to a certain temperature; (3) after the materials are heated to a proper temperature, stopping heating, and starting a waste gas pumping system; (4) the heating box is opened, the materials are moved into the barreled material conveying box, the materials are conveyed into the storage tank in a sealing mode through the pump, and the concentrated storage and disposal of partial dangerous waste barreled materials are achieved. The process designs a process method for heating pretreatment of hazardous waste barreled materials, fully considers the complexity of the hazardous waste barreled materials, realizes preheating of the barreled materials, facilitates subsequent conveying, effectively collects waste gas, recycles hot air, and is efficient and environment-friendly.
Description
Technical Field
The invention relates to the field of waste utilization, in particular to a process method for heating pretreatment of hazardous waste barreled materials. .
Background
At present, the hazardous wastes in China are wide in source and various in types, specifically can be divided into 46 types, and can be simply divided into solid, semi-solid and liquid types according to the existing forms, the disposal processes are mainly divided into resource utilization, incineration landfill and cement kiln cooperation, and any disposal process has relative limitation, and the form and the property of the materials determine the subsequent disposal process.
According to data statistics, solid semi-solid state type, particularly heavy oil and distilled residues are mainly used for hazardous waste in China at normal temperature, and the iron bucket and the ton bucket are mainly used for transferring and storing the hazardous waste, so that the treatment and disposal difficulties of subsequent disposal enterprises are caused.
In addition, some heavy gear oils are difficult to flow at normal temperature, and are difficult to store and convey in a centralized manner in comprehensive utilization enterprises, so that the disposal cost is increased, the enterprise benefit is reduced, and the environmental risk is increased.
Patent No. 201620887243.5 heating cabinet, mainly to the barreled material, need airtight, utilize the circulated air to heat, nevertheless this heating cabinet still exists inside not corrosion-resistant, must airtight heating, and the bottom does not set up water conservancy diversion and collection device simultaneously, is not suitable for the heating preliminary treatment of complicated materials such as dangerously useless.
Patent No. 201721569902.2 a barreled material heating cabinet mainly utilizes constant temperature waters, through the intake pipe to the fin heating back, realizes the heating to the barreled material. However, the heating box generates large exhaust gas, and is not suitable for open heating.
Disclosure of Invention
The invention provides a process method for heating pretreatment of hazardous waste barreled materials, which is suitable for pretreatment treatment of various solid semi-solid materials, recycles heat, effectively reduces waste gas generation, saves energy and protects environment.
The technical scheme for realizing the invention is as follows:
a process method for heating pretreatment of hazardous waste barreled materials comprises the following steps:
(1) processing according to the complexity of barreled hazardous waste materials in batches, opening a barrel cover before heating, placing the barrel cover according to a prefabricated tray, and then placing the barrel cover into a heating box;
the prime number barrel is an iron barrel, a plastic barrel or a ton barrel; the prefabricated tray is an iron tray or a wood tray, and preferably an iron tray, so that the heat transfer effect is excellent, and the service life is long;
(2) determining a proper heating temperature according to the early-stage material analysis condition, and opening an internal circulating fan and an overflow valve simultaneously after the material is heated to a certain temperature;
(3) after the materials are heated to a proper temperature, stopping heating, and starting a waste gas pumping system;
(4) the heating box is opened, the top of the heating box is provided with an exhaust curtain, waste gas generated when the heating box is opened is ensured not to overflow, the bottom of the heating box is provided with a diversion trench, materials are moved into the barreled material conveying box, the materials are conveyed into the storage tank in a closed mode through the pump, and concentrated storage and disposal of partial dangerous waste barreled materials are achieved.
The hazardous waste material in the step (1) is a material with poor viscosity and fluidity at normal temperature (a solid semi-solid material with poor fluidity or no fluidity at normal temperature, and has better fluidity when heated to a certain temperature), such as barreled heavy gear oil, partial rectification residue and the like.
The heating temperature in the step (2) is 60-120 ℃, and the heating mode can be heat conduction oil or steam heating; and after the temperature of the material is raised to 40 ℃, opening an internal circulating fan.
And (2) performing anticorrosive spraying treatment on the inner wall of the heating box in the step (1), selecting different anticorrosive materials according to the properties of the treated materials, prolonging the service life of the heating box, and selecting furan resin, epoxy varnish or vinyl resin as the spraying material of the acidic material (with the pH value of between 5 and 7), wherein furan resins are preferred.
The heating cabinet inner structure can set up to individual layer or multilayer structure according to handling material batch quantity and area, preferred bilayer structure so that the material business turn over heating cabinet operation, vertical high temperature resistant anticorrosive variable frequency fan is chooseed for use to the fan, arranges the heating cabinet top in and is equipped with the circulated air passageway, and the accessible is adjusted the circulation amount of wind and is satisfied the temperature control requirement with heat supply temperature, and the circulated air takes out heat supply material heating and heaies up through the coil pipe.
And (3) in the step (2), a flow guide system is arranged on one side of the heating box, a collection system is arranged on the other side of the heating box, an overflow valve is opened periodically, and waste liquid is collected in a flow guide groove of the heating box and then flows out through the overflow valve and is collected.
And (3) when the pressure of the heating box in the step (2) is more than 50KPa, opening the exhaust gas pumping system and keeping the pressure stable within 50 KPa.
And (3) when the temperature of the material is raised to 40 ℃ in the step (2), opening a circulating fan, enabling circulating air to enter from the lower part and enter from the bottom of the heating wire along the side wall circulating air, taking away the heat of the coil pipe, and realizing uniform temperature rise of the material.
And (4) keeping a micro negative pressure in the barreled material conveying box in the step (4), arranging an exhaust curtain at the top of the heating box to ensure that waste gas generated when the heating box is opened is not overflowed, arranging a diversion trench at the bottom, arranging a heating coil in the storage tank, and ensuring that the temperature in the storage tank is not lower than 80 ℃.
The invention has the beneficial effects that: the heating pretreatment and conveying facility for hazardous waste barrel-contained materials provided by the invention has the advantages of strong operability, cyclic use and utilization rate of heat, no overflow of waste gas, efficient collection, reduction of the utilization difficulty of hazardous waste disposal and utilization enterprises, energy conservation, consumption reduction, reduction of the subsequent operation cost of disposal enterprises and avoidance of the risk of environmental pollution.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts.
FIG. 1 is a simplified schematic of a heating chamber of the present invention.
Wherein, 1-heating box bottom, 2-heating coil, 3-heated air circulation fan, 4-air curtain, 5-bracket, 6-waste gas fan.
Detailed Description
The technical solutions of the present invention will be described clearly and completely with reference to the following embodiments of the present invention, and it should be understood that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be obtained by a person skilled in the art without inventive effort based on the embodiments of the present invention, are within the scope of the present invention.
Example 1
A process method for heating and pretreating barreled hazardous waste heavy gear oil materials comprises the following steps: wherein the heating boxes are arranged in double-layer 4 groups, and the quantity of the materials which can be heated in one time is 64 barrels (200 l iron barrels).
The material is semisolid at normal temperature, the mechanical pump conveying is difficult, but when the material is heated to 80 ℃, the fluidity is good, and the material is convenient to convey and carry out subsequent treatment.
Step (1): reasonably placing barreled heavy gear oil according to the size of the tray, then opening the barrel cover, and moving the barrel cover into the heating box to ensure that the storage capacity of the barreled material cannot be higher than three-quarters of the height of the barrel;
(2) set up the heating cabinet temperature to 85 ℃, utilize the conduction oil to heat, heat conduction oil pipe has been arranged to heater wire inside wall and bottom 1, when the material heaies up to 40 ℃, opens heated air circulation fan 3, and the circulated air gets into from the lower part, and follow the lateral wall circulated air and get into from the heating cabinet bottom, takes away the heat of heating coil bottom and lateral part, realizes the even intensification to the material. Simultaneously, opening an overflow valve at regular time and checking whether the material leaks or not;
(3) the pressure in the box is increased in the heating process, the pressure condition is observed, and the exhaust gas pumping system is properly started to ensure that the pressure in the box is stable and is kept within 50 KPa;
(4) when the materials are heated to 85 ℃ and maintained for 30min, stopping heating, starting a waste gas pumping system, leading the waste gas to a disposal facility, and ensuring that the waste gas does not overflow;
(5) and (3) opening the heating box, moving the materials into the barreled material conveying box by using a forklift, simultaneously opening a waste gas system (a waste gas fan 6) at the top of the conveying box, conveying the materials into the storage tank by using a pump, wherein the heat tracing temperature in the storage tank is not lower than 80 ℃, and ensuring that the materials are conveyed to the next procedure safely.
After the method is adopted, a large amount of barreled materials can be collected and stored in a centralized way, so that the storage and use area is greatly reduced, and the subsequent treatment of enterprises is facilitated. Meanwhile, the heating method is adopted to uniformly heat the materials, effectively shortens the heating time and reduces the heating time by 40 percent compared with the original direct heat transfer; by means of heated air circulation heating, the heat utilization is more sufficient, the heating temperature is controllable and adjustable, the heat utilization efficiency is higher, and the heat utilization efficiency is improved by 30% compared with that of the heating device in the patent 201721569902.2.
Example 2
A process method for heating and pretreating barrel-packed hazardous waste rectification residue materials comprises the following steps: wherein the heating boxes are arranged in double-layer 2 groups, and the quantity of the materials which can be heated at one time is 32 barrels (200 l iron barrels) or 16 barrels (plastic ton barrels).
The material is semisolid viscous at normal temperature, the machine pump cannot convey feeding or store the feeding in a centralized manner, so that the feeding difficulty of enterprises is caused, but when the material is heated to 90 ℃, the fluidity is good, and the transportation and the subsequent treatment are convenient.
Step (1): reasonably placing the barreled rectification residues according to the size of the tray, then opening the barrel cover, and moving the barrel cover into the heating box to ensure that the storage capacity of the barreled materials cannot be higher than three-quarters of the height of the barrel;
(2) set up the heating cabinet temperature to 95 ℃, utilize the conduction oil to heat, heat conduction oil pipe has been arranged to heating cabinet inside wall and bottom, when the material heaies up to 40 ℃, opens circulating fan, and the circulated air gets into from the lower part, and follow the lateral wall circulated air and get into from the heating cabinet bottom, takes away the coil pipe heat, realizes evenly rising temperature to the material. Simultaneously, opening an overflow valve at regular time and checking whether the material leaks or not;
(3) the pressure in the box is increased in the heating process, the pressure condition is observed, and the exhaust gas pumping system is properly started to ensure that the pressure in the box is stable and is kept within 50 KPa;
(4) when the materials are heated to 95 ℃ and maintained for 30min, stopping heating, starting a waste gas pumping system, leading the waste gas to a disposal facility, and ensuring that the waste gas does not overflow;
(5) and opening the heating box, moving the materials into the barreled material conveying box by using a forklift, simultaneously opening a waste gas system at the top of the conveying box, conveying the materials into the storage tank by using a pump, wherein the heat tracing temperature in the storage tank is not lower than 80 ℃, and ensuring that the materials are safely conveyed to the next procedure.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (8)
1. A process method for heating pretreatment of hazardous waste barreled materials is characterized by comprising the following steps:
(1) according to the complexity of barreled hazardous waste materials, processing according to batches, opening a barrel cover before heating, and putting the barrel cover into a heating box;
(2) determining a proper heating temperature according to the early-stage material analysis condition, and opening an internal circulating fan and an overflow valve simultaneously after the material is heated to a certain temperature;
(3) after the materials are heated to a proper temperature, stopping heating, and starting a waste gas pumping system;
(4) the heating box is opened, the materials are moved into the barreled material conveying box, the materials are conveyed into the storage tank in a sealing mode through the pump, and the concentrated storage and disposal of partial dangerous waste barreled materials are achieved.
2. The process for the thermal pretreatment of hazardous waste drums of claim 1, wherein: the hazardous waste material in the step (1) is a material with poor viscosity and fluidity at normal temperature.
3. The process for the thermal pretreatment of hazardous waste drums of claim 1, wherein: the heating temperature in the step (2) is 60-120 ℃, and the heating mode can be heat conduction oil or steam heating; and after the temperature of the material is raised to 40 ℃, opening an internal circulating fan.
4. The process for the thermal pretreatment of hazardous waste drums of claim 1, wherein: and (2) performing anticorrosive spraying treatment on the inner wall of the heating box in the step (1), wherein the spraying material of the acidic material is furan resin, epoxy varnish or vinyl resin.
5. The process for the thermal pretreatment of hazardous waste drums of claim 1, wherein: and (3) in the step (2), a flow guide system is arranged on one side of the heating box, a collection system is arranged on the other side of the heating box, an overflow valve is opened periodically, and waste liquid is collected in a flow guide groove of the heating box and then flows out through the overflow valve and is collected.
6. The process for the thermal pretreatment of hazardous waste drums of claim 1, wherein: and (3) when the pressure of the heating box in the step (2) is more than 50KPa, opening the exhaust gas pumping system and keeping the pressure stable within 50 KPa.
7. The process for the thermal pretreatment of hazardous waste drums of claim 1, wherein: and (3) when the temperature of the material is raised to 40 ℃ in the step (2), opening a circulating fan, enabling circulating air to enter from the lower part and enter from the bottom of the heating wire along the side wall circulating air, taking away the heat of the coil pipe, and realizing uniform temperature rise of the material.
8. The process for the thermal pretreatment of hazardous waste drums of claim 1, wherein: and (4) keeping a micro negative pressure in the barreled material conveying box in the step (4), arranging a heating coil in the storage tank, and keeping the temperature in the storage tank not lower than 80 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011138612.9A CN112128977B (en) | 2020-10-22 | 2020-10-22 | Process method for heating pretreatment of hazardous waste barreled material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011138612.9A CN112128977B (en) | 2020-10-22 | 2020-10-22 | Process method for heating pretreatment of hazardous waste barreled material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN112128977A true CN112128977A (en) | 2020-12-25 |
| CN112128977B CN112128977B (en) | 2022-07-01 |
Family
ID=73854478
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011138612.9A Active CN112128977B (en) | 2020-10-22 | 2020-10-22 | Process method for heating pretreatment of hazardous waste barreled material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112128977B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112944364A (en) * | 2021-03-19 | 2021-06-11 | 江苏爱科固体废物处理有限公司 | Semi-solid hazardous waste incineration treatment process |
| CN114917843A (en) * | 2022-06-08 | 2022-08-19 | 李艺 | Continuous pyrolysis device with a plurality of energy ball circulating pipes arranged on inner wall of reaction kettle |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000193795A (en) * | 1998-12-28 | 2000-07-14 | Ishikawajima Harima Heavy Ind Co Ltd | Radioactive contaminated material container storage |
| CN201539871U (en) * | 2009-10-30 | 2010-08-04 | 上海蓝鸟环境科技发展有限公司 | Unloading, storing and conveying system devices for industrial paste hazardous wastes |
| CN106066041A (en) * | 2016-08-01 | 2016-11-02 | 北京北控环保工程技术有限公司 | Danger wastes pretreatment system |
| CN107238202A (en) * | 2017-06-22 | 2017-10-10 | 中国天辰工程有限公司 | A kind of Lubricating oil barrel dress additive firing equipment and system |
| CN207019080U (en) * | 2017-07-17 | 2018-02-16 | 廊坊开发区富思特工业废弃物收储有限公司 | A kind of pretreatment unit hazardous waste early stage |
| CN108072174A (en) * | 2017-11-29 | 2018-05-25 | 南京新奥环保技术有限公司 | A kind of barreled hazardous waste water bath heating device |
| CN111678138A (en) * | 2020-06-18 | 2020-09-18 | 黑龙江云水环境技术服务有限公司 | Liquid hazardous waste preliminary treatment and waste gas collection device |
-
2020
- 2020-10-22 CN CN202011138612.9A patent/CN112128977B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000193795A (en) * | 1998-12-28 | 2000-07-14 | Ishikawajima Harima Heavy Ind Co Ltd | Radioactive contaminated material container storage |
| CN201539871U (en) * | 2009-10-30 | 2010-08-04 | 上海蓝鸟环境科技发展有限公司 | Unloading, storing and conveying system devices for industrial paste hazardous wastes |
| CN106066041A (en) * | 2016-08-01 | 2016-11-02 | 北京北控环保工程技术有限公司 | Danger wastes pretreatment system |
| CN107238202A (en) * | 2017-06-22 | 2017-10-10 | 中国天辰工程有限公司 | A kind of Lubricating oil barrel dress additive firing equipment and system |
| CN207019080U (en) * | 2017-07-17 | 2018-02-16 | 廊坊开发区富思特工业废弃物收储有限公司 | A kind of pretreatment unit hazardous waste early stage |
| CN108072174A (en) * | 2017-11-29 | 2018-05-25 | 南京新奥环保技术有限公司 | A kind of barreled hazardous waste water bath heating device |
| CN111678138A (en) * | 2020-06-18 | 2020-09-18 | 黑龙江云水环境技术服务有限公司 | Liquid hazardous waste preliminary treatment and waste gas collection device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112944364A (en) * | 2021-03-19 | 2021-06-11 | 江苏爱科固体废物处理有限公司 | Semi-solid hazardous waste incineration treatment process |
| CN114917843A (en) * | 2022-06-08 | 2022-08-19 | 李艺 | Continuous pyrolysis device with a plurality of energy ball circulating pipes arranged on inner wall of reaction kettle |
Also Published As
| Publication number | Publication date |
|---|---|
| CN112128977B (en) | 2022-07-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN112128977B (en) | Process method for heating pretreatment of hazardous waste barreled material | |
| CN104819080B (en) | A kind of marine fuel oil pre-heating mean | |
| CN108860235A (en) | A kind of petroleum residue storage transport device | |
| CN205042861U (en) | Bionics biotechnology handles organic solid waste's intelligent device | |
| CN212222905U (en) | Animal fat refines equipment | |
| CN104773780A (en) | Electroplating heavy metal wastewater zero-discharge/recycling treatment process and dedicated device thereof | |
| CN104150428B (en) | Electronic addition fuel fuel tank cap and its oil transportation method | |
| CN107117614B (en) | Leak-proof environment-friendly vulcanizing device in carbon disulfide production | |
| CN203501672U (en) | Paper-tube drying system | |
| CN204900113U (en) | Boats and ships fuel system of preheating of compulsory convection heat transfer | |
| CN105089872B (en) | The marine fuel oil pre-heating system and its pre-heating mean of forced-convection heat transfer | |
| CN104001338A (en) | Desolventizing system and operation process thereof | |
| CN204984655U (en) | Boats and ships fuel system of preheating based on sleeve pipe form | |
| CN211486601U (en) | Petrochemical detects uses waste gas recovery device | |
| CN205328932U (en) | Automatic trickle heat sink of quenching in low temperature dry distillation furnace | |
| CN210256671U (en) | Novel cement electric pole evaporates foster pond | |
| CN204411751U (en) | A kind of black rosin distilling apparatus | |
| CN202970814U (en) | High-temperature steam waste heat electricity generation energy-saving system | |
| CN206018556U (en) | A kind of industrial heater of environmental protection and energy saving | |
| CN203769898U (en) | Diesel generating set exhaust waste heat assistant driving system | |
| CN206854349U (en) | A kind of total system of kitchen garbage | |
| CN205803038U (en) | A kind for the treatment of tank with heating function | |
| CN205279030U (en) | It recycles and conversion device to pollute high temperature hot water and flash distillation of steam energy | |
| CN205709913U (en) | Waste and old copper-clad plate reaction recovery system | |
| CN221566049U (en) | Needle coke production high-efficiency starting device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |